JP2013166935A5 - - Google Patents

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JP2013166935A5
JP2013166935A5 JP2013025051A JP2013025051A JP2013166935A5 JP 2013166935 A5 JP2013166935 A5 JP 2013166935A5 JP 2013025051 A JP2013025051 A JP 2013025051A JP 2013025051 A JP2013025051 A JP 2013025051A JP 2013166935 A5 JP2013166935 A5 JP 2013166935A5
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JP
Japan
Prior art keywords
gasoline
fractions
light
olefins
mixture
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JP2013025051A
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Japanese (ja)
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JP6111084B2 (en
JP2013166935A (en
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Priority claimed from FR1200424A external-priority patent/FR2986799B1/en
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特許文献3には、低硫黄含有量のガソリンの製造方法であって、ジオレフィンの選択的水素化のための工程と、場合による、ガソリン中に存在する軽質硫黄含有生成物の分子量を増加させることを目的とした、少なくとも1回の工程とを含む、方法が記載されている。この引用特許には、ガソリンを2つのフラクション:軽質ガソリンおよび重質ガソリンに分離することが記載されており、この引用特許は、低硫黄ガソリンを製造するために用いられ得る。
Patent Document 3 discloses a method for producing gasoline having a low sulfur content, which includes a step for selective hydrogenation of diolefins and, optionally, increases the molecular weight of light sulfur-containing products present in gasoline. It aimed, and at least one step, a method has been described. This cited patent describes the separation of gasoline into two fractions: light gasoline and heavy gasoline, which can be used to produce low sulfur gasoline.

場合によっては、軽質ガソリン留分のオリゴマー化は、FCCから、または他の追加の源、例えばコーキング装置から、ビスブレーキングから、メタノールをオレフィンに転換すことから、またはアルコールをオレフィンに転換するための任意の他の方法から、水蒸気分解から、さらにはフィッシャー・トロプシュ(Fischer-Tropsch)合成装置から、またはパラフィンの脱水素から単独でまたは混合物として得られたC3およびC4留分の全てあるいは一部との混合物として行われてもよい。
In some cases, light gasoline fractions oligomerization, the FCC or other additional sources, for example from the coking unit, converted from visbreaking, since you convert methanol to olefins, or alcohols to olefins All or one of the C3 and C4 fractions obtained from any other method for the production, from steam cracking, from a Fischer-Tropsch synthesizer, or from paraffin dehydrogenation alone or as a mixture It may be carried out as a mixture with the part.

JP2013025051A 2012-02-15 2013-02-13 Catalytic cracker and process for converting heavy feedstock using selective hydrogenation process of gasoline obtained from catalytic cracking Active JP6111084B2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR1200424 2012-02-15
FR1200424A FR2986799B1 (en) 2012-02-15 2012-02-15 HEAVY LOAD CONVERTING METHOD USING CATALYTIC CRACKING UNIT AND SELECTIVE HYDROGENATION STEP FROM CATALYTIC CRACKING GASOLINE

Publications (3)

Publication Number Publication Date
JP2013166935A JP2013166935A (en) 2013-08-29
JP2013166935A5 true JP2013166935A5 (en) 2016-03-31
JP6111084B2 JP6111084B2 (en) 2017-04-05

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JP2013025051A Active JP6111084B2 (en) 2012-02-15 2013-02-13 Catalytic cracker and process for converting heavy feedstock using selective hydrogenation process of gasoline obtained from catalytic cracking

Country Status (10)

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US (1) US9249364B2 (en)
EP (1) EP2636661B1 (en)
JP (1) JP6111084B2 (en)
FR (1) FR2986799B1 (en)
HR (1) HRP20211585T1 (en)
MY (1) MY163508A (en)
PH (1) PH12013000053B1 (en)
PL (1) PL2636661T3 (en)
RU (1) RU2617688C2 (en)
TW (1) TWI482849B (en)

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US9982204B2 (en) * 2013-06-13 2018-05-29 Uop Llc Process for producing a chemical feedstock and apparatus relating thereto
CN104549431B (en) * 2013-10-23 2018-06-19 中国石油化工股份有限公司 A kind of preparation method containing sour modified molecular screen hydrocracking catalyst
US9914884B2 (en) 2013-12-17 2018-03-13 Uop Llc Process and apparatus for recovering oligomerate
US9387413B2 (en) 2013-12-17 2016-07-12 Uop Llc Process and apparatus for recovering oligomerate
JP6234829B2 (en) * 2014-01-24 2017-11-22 Jxtgエネルギー株式会社 Fluid catalytic cracking of heavy oil
JP7311831B2 (en) 2014-12-09 2023-07-20 秋吉 神村 Information label
US11566182B2 (en) 2020-03-30 2023-01-31 Chevron U.S.A. Inc. Circular economy for plastic waste to polyethylene via refinery FCC feed pretreater and FCC units
CN115477957A (en) * 2021-05-31 2022-12-16 北京化工大学 Method for reducing olefin content in gasoline

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FR1004585A (en) 1948-05-18 1952-03-31 Waterproof hairstyle and clothing for bad weather
US2945906A (en) * 1955-10-15 1960-07-19 Basf Ag Cracking of oligomers of isobutene in the presence of silica-magnesia catalysts
DE3914817C2 (en) * 1989-05-05 1995-09-07 Huels Chemische Werke Ag Process for oligomerizing olefins
US4973790A (en) * 1989-11-16 1990-11-27 Mobil Oil Corporation Process for upgrading light olefinic streams
DE69012295T2 (en) * 1989-11-16 1995-01-05 Mobil Oil Corp Process for increasing the quality of light olefin streams.
US5202015A (en) * 1991-01-22 1993-04-13 Mobil Oil Corporation Process for distillate dewaxing coincident with light olefin oligomerization
DE69507598T2 (en) * 1994-02-22 1999-09-02 Exxon Chemical Patents Inc OLIGOMERIZATION AND CATALYST DAFUER
US6803494B1 (en) * 1998-05-05 2004-10-12 Exxonmobil Chemical Patents Inc. Process for selectively producing propylene in a fluid catalytic cracking process
US6024865A (en) * 1998-09-09 2000-02-15 Bp Amoco Corporation Sulfur removal process
FR2797639B1 (en) 1999-08-19 2001-09-21 Inst Francais Du Petrole PROCESS FOR PRODUCING LOW SULFUR ESSENCE
FR2837213B1 (en) * 2002-03-15 2004-08-20 Inst Francais Du Petrole PROCESS FOR THE JOINT PRODUCTION OF PROPYLENE AND GASOLINE FROM A RELATIVELY HEAVY LOAD
FR2879620B1 (en) * 2004-12-21 2007-02-23 Inst Francais Du Petrole PROCESS FOR THE DIRECT CONVERSION OF A CHARGE COMPRISING FOUR AND / OR FIVE ATOMIC CARBON OLEFINS FOR THE PRODUCTION OF PROPYLENE WITH CO-PRODUCTION OF GASOLINE
FR2895416B1 (en) 2005-12-22 2011-08-26 Inst Francais Du Petrole SELECTIVE HYDROGENATION PROCESS USING A SULFIDE CATALYST
FR2935377B1 (en) 2008-08-29 2013-02-15 Inst Francais Du Petrole PROCESS FOR CONVERTING A HEAVY FUEL AND PROPYLENE LOAD HAVING A MODULATE YIELD STRUCTURE
FR2935389B1 (en) 2008-09-04 2012-05-11 Inst Francais Du Petrole SELECTIVE HYDROGENATION PROCESS USING SULFIDE CATALYST OF SPECIFIC COMPOSITION
FR2959748B1 (en) * 2010-05-06 2012-05-18 Inst Francais Du Petrole CATALYTIC CRACKING PROCESS WITH RECYCLED OF OLEFIN CUT FROM THE GAS SEPARATION SECTION TO MAXIMIZE PRODUCTION OF PROPYLENE.
FR2964389A1 (en) * 2010-09-07 2012-03-09 IFP Energies Nouvelles PROCESS FOR PRODUCING KEROSENE AND DIESEL FUELS FROM UNSATURATED UNSATURATED CUTTINGS AND AROMATIC CUTTINGS RICH IN BTX
FR2968010B1 (en) * 2010-11-25 2014-03-14 Ifp Energies Now METHOD FOR CONVERTING A HEAVY LOAD TO MEDIUM DISTILLATE

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